Dual component chromia silicate cracking catalyst

Claim 2

A process for catalytically cracking a hydrocarbonaceous feedstock comprising the step of contacting the feedstock in a reaction zone under catalytic cracking conditions in the absence of added hydrogen with a catalyst composition comprising an essentially alumina-free crystalline chromia silicate component having a mole ratio of oxides of SiO 2 :Cr 2 O 3 of greater than about 20:1 and having the random powder X-ray diffraction lines of Table 1, and a large pore size crystalline aluminosilicate cracking component.

Claim 3

The process of claim 1, wherein the large pore size crystalline aluminosilicate cracking component is a Y-type zeolite.

Claim 4

The process of claim 1, wherein the large pore size crystalline aluminosilicate cracking component is an ultra-stable Y-type zeolite.

Claim 5

The process of claim 1, wherein the crystalline chromia silicate component has a composition expressed in the anhydrous state in terms of moles of oxides comprising: R.sub.2 O:aM.sub.2 O:bCr.sub.2 O.sub.3 :cSiO.sub.2 wherein R 2 O is a quaternary alkylammonium oxide, M is an alkali metal selected from the group consisting of lithium, sodium, potassium and their mixtures, a is greater than 0 but less than 1.5, c is greater than or equal to 12, and c/b is greater than about 20; said chromia silicate having the random X-ray diffraction pattern of Table 1.

Claim 6

The process of claim 1, wherein the catalytic cracking conditions include a temperature of from about 425° to 650° C., a pressure from 0 to about 6 atmospheres, a catalyst hydrocarbon weight ratio of from about 2 to 15, and a contact time of from about 0.3 to 10 seconds.

Claim 7

The process of claim 1, wherein the catalyst composition comprises a physical mixture of the two components.

Claim 8

The process of claim 1, wherein the two catalyst components are incorporated is an inorganic matrix.

Claim 9

The process of claim 7, wherein the total weight of the catalyst components is from about 10 to 65 weight percent of the entire composition.

Claim 10

The process of claim 1, wherein the weight ratio of the crystalline chromia silicate component to the crystalline aluminosilicate cracking component is from about 1:20 to 3:1.

Claim 11

A process for catalytically cracking a hydrocarbonaceous feedstock comprising the step of contacting the feedstock under catalytic cracking conditions in a reaction zone in the absence of added hydrogen with a catalyst composition comprising an essentially alumina-free crystalline chromia silicate component having an internal pore structure which will allow entry of normal aliphatic and slightly branched aliphatic compounds, yet substantially exclude all compounds having a molecular dimension equal to or substantially greater than a quaternary carbon atom and at least one large pore size crystalline aluminosilicate cracking component.

Claim 12

A process for catalytically cracking a hydrocarbonaceous feedstock comprising the step of contacting the feedstock under catalytic cracking conditions in a reaction zone in the absence of added hydrogen with a catalyst composition comprising an essentially alumina-free crystalline chromia silicate component having an internal pore structure which will allow entry of normal aliphatic and slightly branched aliphatic compounds, yet substantially exclude all compounds having a molecular dimension equal to or substantially greater than a quaternary carbon atom and at least one large pore size crystalline aluminosilicate cracking component.

Claim 13

The process of claim 10, wherein the weight ratio of the crystalline chromia silicate component to the crystalline aluminosilicate cracking component is from about 1:20 to 3:1.

Claim 14

The process of claim 10, wherein the crystalline chromia silicate component has a mole ratio of oxides SiO 2 Cr 2 O 3 of greater than about 20:1 and the random powder X-ray diffraction lines of Table 1.

Claim 15

The process of claim 10, wherein the large pore crystalline aluminosilicate cracking component is a Y-type zeolite.

Claim 16

The process of claim 10, wherein the large pore crystalline aluminosilicate cracking component is an ultra-stable Y-type zeolite.

Claim 17

The process of claim 10, wherein the catalytic cracking conditions include a temperature of from about 425° to 650° C., a pressure from about 0 to 6 atmospheres, and a contact time in the reaction zone of from about 0.3 to 10 seconds.

Claim 18

The process of claim 10, conducted in a single stage with a single feedstock.

Claim 19

The process of claim 10, wherein the catalyst composition comprises a physical mixture of the two catalyst components.

Claim 20

The process of claim 10, wherein the two catalyst components are incorporated in an inorganic matrix.

Claim 21

The process of claim 18, wherein the total weight of the two catalyst components is from about 10 to 65 weight percent of the entire composition.